EP1843362B1 - Lithiumionenkondensator - Google Patents

Lithiumionenkondensator Download PDF

Info

Publication number
EP1843362B1
EP1843362B1 EP05805234A EP05805234A EP1843362B1 EP 1843362 B1 EP1843362 B1 EP 1843362B1 EP 05805234 A EP05805234 A EP 05805234A EP 05805234 A EP05805234 A EP 05805234A EP 1843362 B1 EP1843362 B1 EP 1843362B1
Authority
EP
European Patent Office
Prior art keywords
positive electrode
negative electrode
lithium
carbonate
lithium ion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP05805234A
Other languages
English (en)
French (fr)
Other versions
EP1843362A4 (de
EP1843362A1 (de
Inventor
Kohei Fuji Jukogyo Kabushiki Kaisha MATSUI
Risa Fuji Jukogyo Kabushiki Kaisha TAKAHATA
Nobuo Fuji Jukogyo Kabushiki Kaisha ANDO
Atsuro Fuji Jukogyo Kabushiki Kaisha SHIRAKAMI
Shinichi Fuji Jukogyo Kabushiki Kaisha TASAKI
Yukinori Fuji Jukogyo Kabushiki Kaisha HATO
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Subaru Corp
Original Assignee
Fuji Jukogyo KK
Fuji Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Jukogyo KK, Fuji Heavy Industries Ltd filed Critical Fuji Jukogyo KK
Publication of EP1843362A1 publication Critical patent/EP1843362A1/de
Publication of EP1843362A4 publication Critical patent/EP1843362A4/de
Application granted granted Critical
Publication of EP1843362B1 publication Critical patent/EP1843362B1/de
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/04Hybrid capacitors
    • H01G11/06Hybrid capacitors with one of the electrodes allowing ions to be reversibly doped thereinto, e.g. lithium ion capacitors [LIC]
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22Electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/22Electrodes
    • H01G11/30Electrodes characterised by their material
    • H01G11/50Electrodes characterised by their material specially adapted for lithium-ion capacitors, e.g. for lithium-doping or for intercalation
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/54Electrolytes
    • H01G11/58Liquid electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/54Electrolytes
    • H01G11/58Liquid electrolytes
    • H01G11/60Liquid electrolytes characterised by the solvent
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/54Electrolytes
    • H01G11/58Liquid electrolytes
    • H01G11/64Liquid electrolytes characterised by additives
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/66Current collectors
    • H01G11/70Current collectors characterised by their structure
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/54Electrolytes
    • H01G11/58Liquid electrolytes
    • H01G11/62Liquid electrolytes characterised by the solute, e.g. salts, anions or cations therein
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01GCAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
    • H01G11/00Hybrid capacitors, i.e. capacitors having different positive and negative electrodes; Electric double-layer [EDL] capacitors; Processes for the manufacture thereof or of parts thereof
    • H01G11/74Terminals, e.g. extensions of current collectors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/13Energy storage using capacitors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/60Other road transportation technologies with climate change mitigation effect
    • Y02T10/70Energy storage systems for electromobility, e.g. batteries

Definitions

  • the present invention relates to a lithium ion capacitor comprising a positive electrode, a negative electrode and an aprotic organic solvent electrolytic solution of a lithium salt as an electrolyte.
  • the lithium ion secondary battery is a so-called rocking chair battery such that after it is assembled, lithium ions are supplied from the lithium-containing metal oxide as the positive electrode to the negative electrode by charging the battery, and the lithium ions in the negative electrode are returned to the positive electrode by discharging the battery, and is characterized by having a high voltage, a large capacity and high safety.
  • lithium ion secondary battery As such a new electrical storage device, attention has been paid to the above lithium ion secondary battery and an electric double layer capacitor.
  • a lithium ion secondary battery Although a lithium ion secondary battery has a high energy density, it still has problems in output characteristics, safety and cycle life.
  • an electric double layer capacitor has been used as a memory backup power source for IC or LSI, but the discharge capacity per charge is small as compared with a battery.
  • it is maintenance-free and has high output characteristics which the lithium ion secondary battery does not have, such as excellent instantaneous charge and discharge characteristics and durability against charge and discharge for several tens of thousands cycles or more.
  • an energy density of a conventional electric double layer capacitor usually ranges from about 3 to about 4 Wh/l, which is lower than by two orders than that of a lithium ion secondary battery.
  • an energy density of from 6 to 10 Wh/l is required for practical use and an energy density of 20 Wh/l for wide spread use.
  • a hybrid capacitor As an electrical storage device to be used for such an application which requires a high energy density and high output characteristics, attention has been paid to an electrical storage device also called a hybrid capacitor comprising a combination of storage principles of a lithium ion secondary battery and an electric double layer capacitor in recent years.
  • a hybrid capacitor usually employs a polarized electrode for the positive electrode and a non-polarized electrode for the negative electrode, and attracts attention as an electrical storage device having both high energy density of a battery and high output characteristics of an electric double layer capacitor.
  • Patent Documents 1 to 4 a hybrid capacitor has been proposed (Patent Documents 1 to 4) in which a negative electrode capable of absorbing and desorbing lithium ions is brought into contact with lithium metal so that lithium ions are preliminarily made to be absorbed and supported (hereinafter sometimes referred to as doping) by the negative electrode by a chemical or electrochemical method to lower the negative electrode potential, thereby to increase the withstand voltage and to significantly increase the energy density.
  • Such a hybrid capacitor is expected to shoe high performance, but has drawbacks such that when the negative electrode is doped with lithium ions, the doping requires a very long time, and it tends to be difficult to uniformly dope the entire negative electrode. Particularly, the doping is practically impossible to be carried out a large-size large capacity cell such as a cylindrical apparatus having electrodes wound or a rectangular battery having a plurality of electrodes laminated.
  • Patent Document 5 an invention such that the entire negative electrodes in the cell can be doped with lithium ions only by disposing lithium metal at the end of the cell, by forming pores penetrating from the front surface to the back surface on each of a negative electrode current collector and a positive electrode current collector so that lithium ions can move via the through pores, and further, by short circuiting the lithium metal as a lithium ion supply source and the negative electrode.
  • Patent Document 5 discloses to conduct similarly the doping on the positive electrode together with the negative electrode or instead of the negative electrode.
  • a lithium ion capacitor according to the preamble of claim 1 is known from EP 1 400 996 A1 .
  • the present inventors have conducted extensive studies and as a result, found the following. Namely, in a lithium ion capacitor wherein a negative electrode and/or a positive electrode is preliminarily doped with lithium ions so that the potentials of the positive electrode and the negative electrode are at most 2.0 V after the positive electrode and the negative electrode are short-circuited, physical properties of an aprotic organic solvent electrolyte solution of a lithium salt to be used closely relate to durability of the obtained capacitor, and the above object can be achieved by incorporating vinylene carbonate or its derivative in the electrolytic solution preferably in an amount of at most 5 wt%.
  • the present invention has been accomplished on the basis of this discovery.
  • the present invention provides the following.
  • a particularly large capacity lithium ion capacitor wherein a negative electrode and/or a positive electrode is preliminarily doped with lithium ions, which has a high energy density and a high output density and further has a high capacity retention during continuous charging at a high temperature and is excellent in durability, is provided.
  • the mechanism how a capacitor has a high energy density and a high output density and further has an improved capacity retention during continuous charging at a high temperature, by incorporating vinylene carbonate in the above electrolytic solution is not necessarily clearly understood but is estimated as follows.
  • Vinylene carbonate has a high reductive decomposition potential and dominates the reductive decomposition on the negative electrode and forms a stable and high quality surface coating film, and thereby suppresses decomposition of other solvents.
  • vinylene carbonate undergoes reductive decomposition to form a coating film on the negative electrode in the initial charging, but since vinylene carbonate has a low oxidation potential, oxidative decomposition on the positive electrode occurs simultaneously, thus causing a problem such as evolution of gas.
  • the positive electrode potential will not increase during the doping, but only the negative electrode potential decreases, whereby no oxidative decomposition of vinylene carbonate on the positive electrode will occur.
  • the positive electrode potential will not increase during the doping, but only the negative electrode potential decreases, whereby no oxidative decomposition of vinylene carbonate on the positive electrode will occur.
  • only formation of a coating film by the reductive decomposition on the negative electrode will occur without any problem such as evolution of gas.
  • the lithium ion capacitor of the present invention comprises a positive electrode, a negative electrode and an aprotic organic electrolytic solution of a lithium salt as an electrolytic solution, wherein a positive electrode active material is a material capable of reversively supporting lithium ions and/or anions, and a negative electrode active material is a material capable of reversively supporting lithium ions.
  • a positive electrode active material is a material capable of reversively supporting lithium ions and/or anions
  • a negative electrode active material is a material capable of reversively supporting lithium ions.
  • the "positive electrode” means an electrode on the side where a current flows out at the time of discharge
  • the "negative electrode” means an electrode on the side where a current flows in at the time of discharge.
  • the potential of the positive electrode is at most 2.0 V after the positive electrode and the negative electrode are short-circuited by doping of the negative electrode and/or the positive electrode with lithium ions.
  • the potentials of the positive electrode and the negative electrode are both 3 V, and the potential of the positive electrode is 3 V after the positive electrode and the negative electrode are short-circuited.
  • the potential of the positive electrode being at most 2.0 V after the positive electrode and the negative electrode are short-circuited means a potential of the positive electrode of at most 2.0 V as obtained by either of the following two methods (A) and (B). That is, (A) after doping with lithium ions, a positive electrode terminal and a negative electrode terminal of a capacitor cell are directly connected by a conducting wire and the capacitor is left to stand for at least 12 hours in such a state, and then the short circuit is released, and the positive electrode potential is measured within from 0.5 to 1.5 hours, (B) after discharging to 0 V at a constant current over a period of at least 12 hours by a charge and discharge testing apparatus, a positive electrode terminal and a negative electrode terminal are connected by a conducting wire and the capacitor is left to stand for at least 12 hours in such a state, and then the short circuit is released, and the positive electrode potential is measured within from 0.5 to 1.5 hours.
  • the positive electrode potential being at most 2.0 V after the positive electrode and the negative electrode are short-circuited is not limited only to the potential immediately after doping with lithium ions, but means a positive electrode potential of at most 2.0 V after short circuit in any state, i.e. short circuit in a charged state, in a discharged state or after repeated charging and discharging.
  • the positive electrode potential being at most 2.0 V after the positive electrode and the negative electrode are short-circuited, will be described in detail below.
  • an activated carbon and a carbon material usually have a potential at a level of 3 V (Li/Li + ).
  • both potentials are about 3 V, the positive electrode potential will be unchanged and about 3 V even when the electrodes are short-circuited.
  • the positive electrode potential will be unchanged and about 3 V even when the electrodes are short-circuited.
  • the negative electrode potential will move to the vicinity of 0 V by charge although it depends on the balance of positive electrode and negative electrode weights, and it is thereby possible to increase the charging voltage, whereby a capacitor having a high voltage and a high energy density will be obtained.
  • the upper limit of the charging voltage is determined to be a voltage at which no decomposition of the electrolytic solution by an increase of the positive electrode potential will occur.
  • the positive electrode potential when the positive electrode potential is at the upper limit, it is possible to increase the charging voltage correspondingly to a decrease of the negative electrode potential.
  • the upper limit potential of the positive electrode is 4.0 V for example, the positive electrode potential at the time of discharge is limited to 3.0 V, and the change in the potential of the positive electrode is at 1.0 V and the capacity of the positive electrode can not sufficiently be utilized.
  • the initial charge and discharge efficiency is low in many cases, and some lithium ions can not be released at the time of discharging.
  • the charge and discharge efficiency of the negative electrode tends to be low as compared with the charge and discharge efficiency of the positive electrode, and thus the positive electrode potential will be higher than 3 V when the cell is short-circuited after charging and discharging are repeatedly carried out, and the utilization of the capacity will further decrease. That is, if the positive electrode is discharged only from 4.0 V to 3.0 V even if it is possible to be discharged from 4.0 V to 2.0 V, only half the capacity is utilized, and the capacitor can not have a large capacity although it may have a high voltage.
  • the positive electrode potential after the short circuit is lower than 3.0 V
  • the utilization of the capacity will increase correspondingly, and a large capacity will be achieved.
  • the positive electrode potential will be at most 2.0 V
  • the lithium ions are supplied other than from the positive electrode and the negative electrode, potentials of the positive electrode, the negative electrode and lithium metal are in equilibrium and at most 3.0 V when the positive and negative electrodes are shortcircuited.
  • the larger the amount of lithium metal the lower the equilibrium potential.
  • the equilibrium potential changes depending upon the negative electrode material and the positive electrode material, it is required to adjust the amount of lithium ions to be supported by the negative electrode considering characteristics of the negative electrode material and the positive electrode material so that the positive electrode potential after short circuit will be at most 2.0 V.
  • the utilized capacity of the positive electrode will be high, whereby a high capacity will be achieved, and a high energy density will be obtained.
  • the larger the amount of lithium ions supplied the lower the positive electrode potential after the positive electrode and the negative electrode are short-circuited and the more the energy density will improve. In order to obtain a further higher energy density, at most 1.5 V is preferred, and particularly at most 1.0 V is more preferred.
  • the positive electrode potential will be higher than 2.0 V when the positive electrode and the negative electrode are short-circuited, and the energy density of the cell tends to be low. Further, if the positive electrode potential after short circuit is less than 1.0 V, drawbacks such as evolution of gas or irreversible consumption of lithium ions may occur depending upon the positive electrode active material, and it tends to be difficult to measure the positive electrode potential. Further, a too low positive electrode potential means an excessive weight of the negative electrode, and the energy density will rather decrease. It is usually at least 0.1 V, preferably at least 0.3 V.
  • one of or both the negative electrode and the positive electrode may be doped with lithium ions.
  • an activated carbon is used for the positive electrode for example, if the amount of lithium ions doped is large and the positive electrode potential is low, lithium ions may be irreversibly consumed, and drawbacks such as a decrease in the capacity of the cell may occur in some cases.
  • doping with lithium ions is conducted preferably on the negative electrode since it makes the process complicated to control the amount of doping the positive electrode and the amount of doping the negative electrode.
  • a high voltage and large capacity capacitor will be obtained particularly when the capacitance per unit weight of the negative electrode active material is at least three times the capacitance per unit weight of the positive electrode active material and when the weight of the positive electrode active material is larger than the weight of the negative electrode active material.
  • a negative electrode having a large capacitance per unit weight relative to the capacitance per unit weight of the positive electrode it becomes possible to reduce the negative electrode active material weight without changing the change in potential of the negative electrode, whereby the amount of the positive electrode active material charged tends to increase, whereby the capacitance and the capacity of the cell can be increased.
  • the positive electrode active material weight is preferably larger than the negative electrode active material weight, and it is more preferably from 1.1 times to 10 times. If it is less than 1.1 times, the difference in capacity with an electric double layer capacitor tends to be small, and if it exceeds 10 times, the capacity may be small on the contrary in some cases, and the difference in thickness between the positive electrode and the negative electrode will be too significant, and such is unfavorable in view of the cell structure.
  • the capacitance and the capacity of the capacitor cell are defined as follows.
  • the capacitance of a cell represents the electrical quantity applied to the cell per unit voltage of the cell (slope of the discharge curve) and its unit is F (farad).
  • the capacitance per unit weight of a cell is a value obtained by dividing the capacitance of the cell by a total weight of the positive electrode active material and the negative electrode active material in the cell and its unit is F/g.
  • the capacitance of a positive electrode or a negative electrode represents the electrical quantity applied to the cell per unit voltage of the positive electrode or the negative electrode (slope of the discharge curve) and its unit is F.
  • the capacitance per unit weight of a positive electrode or a negative electrode represents a value obtained by dividing the capacitance of the positive electrode or the negative electrode by the weight of the positive electrode or the negative electrode active material in the cell and its unit is F/g.
  • the cell capacity is a product of the capacitance of a cell and a difference between the discharge starting voltage and the discharge completion voltage of a cell i.e. a change in voltage, and its unit is C (coulomb).
  • 1C is charge quantity when 1A current is applied in one second, and thus the unit is calculated as mAh in the present invention.
  • the positive electrode capacity is a product of the capacitance of the positive electrode and a difference (a change in positive electrode potential) between the positive electrode potential when discharge starts and the positive electrode potential when discharge is completed, and its unit is C or mAh.
  • the negative electrode capacity is a product of the capacitance of the negative electrode and a difference (change in negative electrode potential) between the negative electrode potential when discharge starts and the negative electrode potential when discharge is completed, and its unit is C or mAh.
  • the cell capacity agrees with the positive electrode capacity and the negative electrode capacity.
  • a means of preliminarily doping the negative electrode and/or the positive electrode with lithium ions for the lithium ion capacitor of the present invention is not particularly limited.
  • a lithium ion supply source capable of supplying lithium ions, such as metal lithium may be disposed in a capacitor cell as a lithium electrode.
  • the amount of the lithium ion supply source (the weight of e.g. lithium metal) an amount with which a predetermined capacity of the negative electrode will be obtained is sufficient.
  • the negative electrode and the lithium electrode may be brought into physical contact (short circuit), or electrochemical doping may be employed.
  • the lithium ion supply source may be formed on a lithium electrode current collector comprising an electrically conductive porous body.
  • the electrically conductive porous body to be the lithium electrode current collector may be a metal porous body which will not react with the lithium ion supply source, such as a stainless steel mesh.
  • a positive electrode current collector and a negative electrode current collector each for receiving and supplying electricity are provided for the positive electrode and the negative electrode, respectively.
  • the lithium electrode is disposed so as to face the negative electrode current collector so that it can electrochemically supply lithium ions to the negative electrode.
  • a material having pores penetrating from the front surface to the back surface, such as an expanded metal is used, and the lithium electrode is disposed to face the negative electrode and/or the positive electrode.
  • the shape, number, etc. of the through pores are not particularly limited and may suitably be set so that lithium ions in an electrolytic solution as described hereinafter can move from the front surface to the back surface of the electrode without being blocked by the electrode current collector.
  • doping with lithium ions can be uniformly carried out also in a case where the lithium electrode for doping the negative electrode and/or the positive electrode is locally disposed in the cell. Accordingly, even in the case of a large capacity cell having the positive electrode and the negative electrode laminated or wound, the negative electrode can be smoothly and uniformly doped with lithium ions by disposing the lithium electrode at a part of the outermost portion of the cell.
  • lithium means a substance containing at least lithium and capable of supplying lithium ions, such as lithium metal or a lithium/aluminum alloy.
  • the aprotic organic solvent electrolyte solution to be used in the lithium ion capacitor of the present invention contains vinylene carbonate from such reasons that a more stable and higher quality coating film can be formed on the surface of the negative electrode.
  • the content of vinylene carbonate in the electrolytic solution has to be preferably at most 5 wt%. If the content is higher than 5 wt%, vinylene carbonate will be present excessively in the electrolytic solution, which may impair cell characteristics such as durability in some cases. Further, if the content is low, its effect expected in the present invention tends to be small, and accordingly it is preferably at least 0.01 wt%, particularly preferably from 0.1 to 3 wt%.
  • the aprotic organic solvent to form the aprotic organic solvent electrolyte solution in the present invention is preferably a cyclic aprotic solvent and/or a chain aprotic solvent.
  • the cyclic aprotic solvent may be a cyclic carbonate such as ethylene carbonate, a cyclic ester such as ⁇ -butyrolactone, a cyclic sulfone such as sulfolane or a cyclic ether such as dioxolane.
  • the chain aprotic solvent may be a chain carbonate such as dimethyl carbonate, a chain carboxylate such as methyl propionate or a chain ether such as dimethoxyethane. These aprotic organic solvents may be a mixture of two or more of them.
  • the aprotic solvent is preferably a mixture of the above cyclic aprotic solvent with the chain aprotic solvent in view of characteristics of the capacitor, and particularly preferably a mixture of a cyclic carbonate with a chain carbonate.
  • the cyclic carbonate may, for example, be ethylene carbonate, propylene carbonate or butylene carbonate.
  • the chain carbonate may, for example, be dimethyl carbonate, methyl ethyl carbonate, diethyl carbonate or methyl propyl carbonate.
  • a preferred combination for the solvent mixture of a cyclic carbonate with a chain carbonate may, for example, be ethylene carbonate and dimethyl carbonate, ethylene carbonate and diethyl carbonate, ethylene carbonate and ethyl methyl carbonate, ethylene carbonate, dimethyl carbonate and diethyl carbonate, ethylene carbonate, diethyl carbonate and methyl ethyl carbonate, ethylene carbonate, dimethyl carbonate and propylene carbonate, ethylene carbonate, methyl ethyl carbonate and propylene carbonate, or ethylene carbonate, diethyl carbonate and propylene carbonate, and particularly preferred is a combination of ethylene carbonate, diethyl carbonate and propylene carbonate.
  • the mixture ratio in the solvent mixture of a cyclic carbonate with a chain carbonate is suitably such that the cyclic carbonate:chain carbonate is preferably from 1:99 to 80:20, more preferably from 10:90 to 60:40.
  • any lithium salt may be used so long as it is an electrolyte capable of forming lithium ions.
  • a lithium salt may, for example, be preferably LiClO 4 , LiAsF 6 , LiBF 4 , LiPF 6 , LiN(C 2 F 5 SO 2 ) 2 or LiN(CF 3 SO 2 ) 2 .
  • Particularly LiPF 6 is suitable, which has a high ionic conductivity and has a low resistance.
  • the above electrolyte and solvent are mixed in a sufficiently dehydrated state to obtain an electrolyte solution.
  • the concentration of the electrolyte in the electrolytic solution is preferably at least 0.1 mol/l so as to reduce the internal resistance contributed from the electrolytic solution, more preferably within a range of from 0.5 to 1.5 mol/l.
  • the positive electrode active material in the lithium ion capacitor of the present invention comprises a material capable of reversively supporting lithium ions and anions such as tetrafluoroborate.
  • a positive electrode active material may be formed by known activated carbon particles.
  • the grain size of the activated carbon can be selected from wide ranges which are generally employed.
  • the 50% volume cumulative diameter (also called D50) is at least 2 ⁇ m, preferably from 2 to 50 ⁇ m, particularly preferably from 2 to 20 ⁇ m.
  • the average pore size is preferably at most 10 nm
  • the specific surface area is preferably from 600 to 3,000 m 2 /g, particularly preferably from 1,300 to 2,500 m 2 /g.
  • the positive electrode in the present invention is formed from the above activated carbon powder by means of a known method. Namely, the activated carbon powder, a binder and if necessary, an electrically conductive agent and a thickener (such as CMC) are dispersed in an aqueous or organic solvent to obtain a slurry, and the slurry is applied on a current collector to be used if necessary, or the slurry is preliminarily formed into a sheet, which is bonded on the current collector.
  • a thickener such as CMC
  • the binder to be used may, for example, be a rubber type binder such as SBR, a fluororesin such as polytetrafluoroethylene or polyvinylidene fluoride, a thermoplastic resin such as a polypropylene or a polyethylene, or an acrylic resin.
  • a rubber type binder such as SBR
  • a fluororesin such as polytetrafluoroethylene or polyvinylidene fluoride
  • a thermoplastic resin such as a polypropylene or a polyethylene
  • acrylic resin acrylic resin
  • the electrically conductive agent to be used if necessary may, for example, be acetylene black, graphite or a metal powder.
  • the amount of the electrically conductive agent to be used varies depending upon the electrical conductivity of the negative electrode active material, the electrode shape, etc., but a proportion of from 2 to 40 wt% based on the negative electrode active material is suitable.
  • the negative electrode active material in the present invention is formed from a material capable of reversively supporting lithium ions.
  • a preferred material may, for example, be a carbon material such as graphite, hard carbon or coke, or a polyacenic material (hereinafter sometimes referred to as PAS).
  • PAS may be one obtained by carbonizing e.g. a phenol resin, activating it if necessary and pulverizing it. The carbonization is carried out by putting the phenol resin or the like in a heating furnace and heating it at a temperature at which it is carbonized for a predetermined time, in the same manner as in the case of the activated carbon for the positive electrode. The temperature varies depending upon e.g. the heating time, and it is usually from 400 to 800°C in the case of PAS.
  • the pulverization is carried out by means of a known pulverizer such as a ball mill.
  • PAS is particularly preferred with a view to obtaining a large capacity.
  • a capacitance of at least 650 F/g will be obtained when lithium ions in an amount of 400 mAh/g are supported (charged) by PAS, and a capacitance of at least 750 F/g will be obtained when lithium ions in an amount of at least 500 mAh/g are charged.
  • PAS has an amorphous structure, and the larger the amount of lithium ions to be supported, the lower the potential.
  • the withstand voltage (charge voltage) of the capacitor to be obtained tends to increase, and the voltage-increasing rate (the slope of the discharge curve) in discharge tends to be low, whereby the capacity will slightly increase. Therefore, it is desirable to set the amount of lithium ions within the lithium ion absorbing power of the active material depending upon the desired working voltage of the capacitor.
  • PAS which has an amorphous structure
  • PAS is free from structural changes such as swelling and contraction upon insertion and release of lithium ions and is thereby excellent in cyclic characteristics. Further, it has an isotropic molecular structure (a higher-order structure) for insertion and release of lithium ions and is thereby excellent in quick charge and quick discharge, and accordingly it is suitable.
  • An aromatic condensed polymer which is a precursor of PAS is a condensed product of an aromatic hydrocarbon compound with an aldehyde.
  • the aromatic hydrocarbon compound may be suitably a so-called phenol such as phenol, cresol or xylenol.
  • x and y which are independent of each other, is 0, 1 or 2, or a hydroxy-bisphenyl or a hydroxynaphthalene.
  • a phenol is suitable.
  • the aromatic condensed polymer may also be a modified aromatic condensed polymer having part of the above aromatic hydrocarbon compound having a phenolic hydroxyl group substituted by an aromatic hydrocarbon compound having no phenolic hydroxyl group such as xylene, toluene or aniline, for example, a condensed product of phenol, xylene and formaldehyde.
  • a modified aromatic polymer substituted by melamine or urea may also be used, and a furan resin is also suitable.
  • PAS is produced as follows. Namely, the above aromatic condensed polymer is gradually heated to an appropriate temperature of from 400 to 800°C in a non-oxidizing atmosphere (including vacuum) to obtain an insoluble and infusible substrate having an atomic ratio of hydrogen atoms/carbon atoms (hereinafter referred to as H/C) of from 0.5 to 0.05, preferably from 0.35 to 0.10.
  • H/C hydrogen atoms/carbon atoms
  • the insoluble and infusible substrate in X-ray diffraction (CuK ⁇ ), the main peak is present at the position of at most 24° as represented by 2 ⁇ , and another broad peak is present at a position of from 41 to 46° in addition to the above main peak.
  • the insoluble and infusible substrate has a polyacenic skeleton structure having an aromatic polycyclic structure appropriately developed, has an amorphous structure, and is capable of being stably doped with lithium ions.
  • the negative electrode active material is formed from negative electrode active material particles having a 50% volume cumulative diameter (also called D50) of from 0.5 to 30 ⁇ m, preferably from 0.5 to 15 ⁇ m, particularly preferably from 0.5 to 6 ⁇ m. Further, the negative electrode active material particles of the present invention have a specific surface area preferably between 0.1 and 2,000 m 2 /g, more preferably between 0.1 and 1,000 m 2 /g, particularly preferably between 0.1 and 600 m 2 /g.
  • the negative electrode in the present invention is formed from the above negative electrode active material powder, by means of a known method in the same manner as in the case of the positive electrode. Namely, the negative electrode active material powder, a binder and if necessary, an electrically conductive agent and a thickener (such as CMC) are dispersed in an aqueous or organic solvent to obtain a slurry, and the slurry is applied on the above current collector, or the slurry is preliminarily formed into a sheet, which is bonded on the current collector.
  • a thickener such as CMC
  • the binder to be used may, for example, be a rubber type binder such as SBR, a fluororesin such as polytetrafluoroethylene or polyvinylidene fluoride, a thermoplastic resin such as a polypropylene or a polyethylene, or an acrylic resin.
  • SBR rubber type binder
  • fluororesin such as polytetrafluoroethylene or polyvinylidene fluoride
  • thermoplastic resin such as a polypropylene or a polyethylene
  • acrylic resin acrylic resin
  • the lithium ion capacitor of the present invention is particularly suitable for a large capacity cell such as a wound type cell comprising strip positive electrode and negative electrode wound with a separator interposed therebetween, a laminate type cell comprising at least three plate-like positive electrodes and at least three plate-like negative electrodes laminated with a separator interposed therebetween, or a film type cell having a laminate comprising at least three plate-like positive electrodes and at least three plate-like negative electrodes laminated with a separator interposed therebetween, sealed in an outer film. Structures of such cells have been already known from e.g. WO00/07255 , WO03/003395 and JP-A-2004-266091 .
  • the capacitor cell of the present invention may have the same structures as those of known cells.
  • a phenol resin molded plate having a thickness of 0.5 mm was put in a Siliconit electric furnace and subjected to a heat treatment by increasing the temperature at a rate of 50°C/hour to 550°C and further at a rate of 10°C/hour to 670°C in a nitrogen atmosphere thereby to synthesize PAS.
  • the PAS plate thus obtained was pulverized with a ball mill to obtain a PAS powder having an average particle size of 4 ⁇ m.
  • the PAS powder had a H/C ratio of 0.2.
  • the slurry for a negative electrode was applied on both sides of copper expanded metal (manufactured by Nippon Metal Industry Co., Ltd.) having a thickness of 32 ⁇ m (porosity 57%) as a negative electrode current collector by a roll coater, followed by vacuum drying to obtain a negative electrode having an entire thickness (the total of the thickness of the negative electrode layers on both sides, the thickness of the electrically conductive layers on both sides and the thickness of the negative electrode current collector) of 89 ⁇ m.
  • a non-aqueous carbon type electrically conductive coating was applied on both sides of aluminum expanded metal (manufactured by Nippon Metal Industry Co., Ltd.) having a thickness of 38 ⁇ m (porosity 47%) by a roll coater and dried to obtain a current collector for a positive electrode having electrically conductive layers formed thereon.
  • the entire thickness (the total of the current collector thickness and the electrically conductive layer thickness) was 52 ⁇ m, and through pores were substantially clogged with the electrically conductive coating.
  • the above slurry for a positive electrode was applied on both sides of the positive electrode current collector by a roll coater, followed by vacuum drying to obtain a positive electrode having an entire thickness (the total of the thickness of the positive electrode layers on both sides, the thickness of the electrically conductive layers on both sides and the thickness of the positive electrode current collector) of 173 ⁇ m.
  • the negative electrode was cut into a negative electrode for evaluation having a size of 1.5x2.0 cm 2 .
  • the negative electrode and lithium metal having a size of 1.5x2.0 cm 2 and a thickness of 200 ⁇ m as an opposite electrode were overlaid with a polyethylene nonwoven fabric having a thickness of 50 ⁇ m as a separator interposed therebetween to assemble a mimic cell.
  • Lithium metal was used as a reference electrode.
  • As an electrolytic solution a solution having LiPF 6 dissolved at a concentration of 1 mol/l in propylene carbonate was used.
  • Lithium ions were charged in an amount of 600 mAh/g based on the negative electrode active material weight at a charge current of 1 mA, and then discharge to 1.5 V was carried out at 1 mA.
  • the capacitance per unit weight of the negative electrode was obtained from the discharge time over which the potential of the negative electrode changed by 0.2 V from the potential which one minute went on after initiation of the discharge, and found to be 912 F/g.
  • the above positive electrode was cut into a positive electrode for evaluation having a size of 1.5x2.0 cm 2 .
  • the positive electrode and lithium metal having a size of 1.5x2.0 cm 2 and a thickness of 200 ⁇ m as an opposite electrode were overlaid with a polyethylene nonwoven fabric having a thickness of 50 ⁇ m as a separator interposed therebetween to assemble a mimic cell.
  • Lithium metal was used as a reference electrode.
  • As an electrolytic solution a solution having LiPF 6 dissolved at a concentration of 1 mol/l in propylene carbonate was used. Charge to 3.6 V at a charge current of 1 mA was carried out and then constant voltage charge was carried out, and after a total charge time of 1 hour, discharge was carried out to 2.5 V at 1 mA.
  • the capacitance per unit weight of the positive electrode was obtained from the discharge time from 3.5 V to 2.5 V and found to be 140 F/g.
  • the positive electrode was cut into five pieces having a size of 2.4 cm ⁇ 3.8 cm, the negative electrode was cut into six pieces having a size of 2.4 cm ⁇ 3.8 cm, and they were laminated with a separator interposed therebetween as shown in Fig. 1 , followed by drying at 150°C for 12 hours, and a separator was disposed on each of the uppermost and lowermost portions, and four sides of the laminate were fixed with a tape to obtain an electrode laminate unit.
  • lithium metal in an amount corresponding to 600 mAh/g based on the weight of the negative electrode active material one having a lithium metal foil having a thickness of 70 ⁇ m contact bonded on copper expanded metal having a thickness of 23 ⁇ m was used, and one sheet was disposed on the outermost portion of the electrode laminate unit to face the negative electrode.
  • the negative electrodes (six sheets) and the stainless steel net having lithium metal contact bonded thereon were welded and contacted to obtain an electrode laminate unit.
  • an aluminum positive electrode terminal On terminal welding portions (five sheets) of the positive electrode current collectors of the above electrode laminate unit, an aluminum positive electrode terminal having a width of 3 mm, a length of 50 mm and a thickness of 0.1 mm, having a sealant film preliminarily heat sealed on a sealing area, and was overlaid and welded by ultrasonic welding.
  • a nickel negative electrode terminal having a width of 3 mm, a length of 50 mm and a thickness of 0.1 mm, having a sealant film preliminarily heat sealed on a sealing area, was overlaid and welded by ultrasonic welding, and the laminate was disposed between one outer film deep-drawn to a size of 60 mm ⁇ 30 mm and 3 mm in depth and one outer film not deep-drawn.
  • Example 1 as the electrolytic solution, a solution having vinylene carbonate added in an amount of 1 wt% to a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared.
  • Example 2 as the electrolytic solution, a solution having vinylene carbonate added in an amount of 3 wt% to a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared.
  • Example 3 as the electrolytic solution, a solution having vinylene carbonate added in an amount of 0.1 wt% to a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared.
  • Example 4 as the electrolytic solution, a solution having vinylene carbonate added in an amount of 0.5 wt% to a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared.
  • Example 5 as the electrolytic solution, a solution having vinylene carbonate added in an amount of 1 wt% to a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate and methyl ethyl carbonate in a weight ratio of 2:3, was used, and three cells were prepared.
  • Example 6 as the electrolytic solution, a solution having vinylene carbonate added in an amount of 1 wt% to a solution having LiN(C 2 F 5 SO 2 ) 2 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared.
  • Comparative Example 1 as the electrolytic solution, a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared.
  • Comparative Example 2 as the electrolytic solution, a solution having LiPF 6 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate and methyl ethyl carbonate in a weight ratio of 2:3, was used, and three cells were prepared.
  • Comparative Example 3 as the electrolytic solution, a solution having LiN(C 2 F 5 SO 2 ) 2 dissolved at a concentration of 1.2 mol/l in a solvent mixture of ethylene carbonate, diethyl carbonate and propylene carbonate in a weight ratio of 3:4:1, was used, and three cells were prepared. '
  • the positive electrodes and the negative electrodes were short-circuited to measure the positive electrode potential, whereupon the positive electrode potential in each Example was within a range of from 0.85 to 0.95 V, which was at most 2.0 V.
  • the other cell of the film type capacitor in each Example was charged at a constant current of 200 mA until the cell voltage became 3.8 V, and then a constant current/constant voltage charge of applying a constant voltage of 3.8 V was carried out for 30 minutes. Then, discharge at a constant current of 200 mA was carried out until the cell voltage became 2.2 V.
  • the initial capacitance and the energy density were calculated from the cell capacity, the discharge starting voltage, the discharge completion voltage and the average voltage after the cycle of from 3.8 V to 2.2 V.
  • a voltage of 3.6 V was applied in a thermostatic chamber of 60°C, and after a certain time, the application of a voltage was terminated, the cell was taken out from the thermostatic chamber and left to stand at 25°C for 3 hours, and the above cycle of from 3.8 V to 2.2 V was carried out to calculate the capacitance, and such a measurement was repeatedly carried out (voltage application test).
  • the capacitance was calculated after a lapse of 60 hours, 173 hours, 333 hours and 1,010 hours after the application of a voltage, thereby to obtain a retention relative to the initial capacitance.
  • Capacitance retention capacitance after a lapse of predetermined time / initial capacitance ⁇ 100
  • VC represents vinylene carbonate, EC ethylene carbonate, DEC diethyl carbonate, PC propylene carbonate and MEC methyl ethyl carbonate.
  • F Energy density (Wh/l) Ex. 1 3EC+4DEC+PC LiPF 6 1 29.7 12.1 Ex. 2 3EC+4DEC+PC LiPF 6 3 29.3 11.9 Ex. 3 3EC+4DEC+PC LiPF 6 0.1 31.5 12.6 Ex. 4 3EC+4DEC+PC LiPF 6 0.5 29.6 12.0 Ex. 5 2EC+3MEC LiPF 6 1 29.9 12.1 Ex.
  • Example 1 wherein 1 wt% of vinylene carbonate was contained, Example 2 wherein 3 wt% of vinylene carbonate was contained, Example 3 wherein 0.1 wt% of vinylene carbonate was contained and Example 4 wherein 0.5 wt% of vinylene carbonate was contained as compared with Comparative Example 1 wherein no vinylene carbonate was contained.
  • Example 5 In a case where ethylene carbonate and methyl ethyl carbonate were used as the solvents and LiPF 6 was used as the solute, the capacity retention after a lapse of 1,010 hours after voltage application at 60°C was high and durability improved in Example 5 wherein 1 wt% of vinylene carbonate was contained as compared with Comparative Example 2 wherein no vinylene carbonate was contained. However, since the capacity retention was low in Example 5 as compared with in Example 1, preferred as the solvent is a mixture of ethylene carbonate, diethyl carbonate and propylene carbonate.
  • the lithium ion capacitor of the present invention is very useful as a driving or auxiliary electrical storage source for electric automobiles, hybrid electric automobiles, etc. Further, it is suitable as a driving storage source for electric automobiles, motorized wheelchairs, etc., an electrical storage device for various energy generation such as solar energy generation or wind power generation, or an electrical storage source for domestic electrical equipment.

Landscapes

  • Engineering & Computer Science (AREA)
  • Power Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Electric Double-Layer Capacitors Or The Like (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Claims (8)

  1. Lithiumionenkondensator, umfassend eine positive Elektrode, eine negative Elektrode und eine Elektrolytlösung eines Lithiumsalzes in einem aprotischen organischen Lösungsmittel als eine elektrolytische Lösung,
    wobei ein aktives Material einer positiven Elektrode ein Material ist, welches befähigt ist, reversibel Lithiumionen und/oder Anionen zu tragen, ein aktives Material einer negativen Elektrode ein Material ist, welches befähigt ist, reversibel Lithiumionen zu tragen,
    wobei die negative Elektrode und/oder die positive Elektrode mit Lithiumionen dotiert sind, so dass das Potential der positiven Elektrode höchstens 2,0 V beträgt, nachdem die positive Elektrode und die negative Elektrode kurzgeschlossen sind, dadurch gekennzeichnet, dass die elektrolytische Lösung Vinylencarbonat enthält.
  2. Lithiumionenkondensator nach Anspruch 1, wobei die positive Elektrode und/oder die negative Elektrode einen Stromabnehmer mit Poren aufweist, die von der vorderen Oberfläche zu der hinteren Oberfläche durchdringen, und durch elektrochemischen Kontakt der negativen Elektrode mit einer Lithiumionenvorratsquelle mit Lithiumionen dotiert sind.
  3. Lithiumionenkondensator nach Anspruch 1 oder 2, wobei das aktive Material der negativen Elektrode eine Kapazität pro Gewichtseinheit aufweist, welche mindestens dreimal die des aktiven Materials der positiven Elektrode beträgt, und das Gewicht des aktiven Materials der positiven Elektrode größer ist als das Gewicht des aktiven Materials der negativen Elektrode.
  4. Lithiumionenkondensator nach einem der Ansprüche 1 bis 3, wobei die elektrolytische Lösung Vinylencarbonat in einer Menge von höchstens 5 Gew.-% enthält.
  5. Lithiumionenkondensator nach einem der Ansprüche 1 bis 4, wobei das aprotische organische Lösungsmittel ein Gemisch eines zyklischen Carbonats mit einem Kettencarbonat ist.
  6. Lithiumionenkondensator nach einem der Ansprüche 1 bis 5, wobei das aprotische organische Lösungsmittel ein Gemisch von Ethylencarbonat, Propylencarbonat und Diethylcarbonat ist.
  7. Lithiumionenkondensator nach einem der Ansprüche 1 bis 6, wobei das Lithiumsalz LiPF6, LiN(C2F5SO2)2 oder LiN(CF3SO2)2 ist.
  8. Lithiumionenkondensator nach einem der Ansprüche 1 bis 7, wobei die positive Elektrode aus Aktivkohlepulver gebildet ist.
EP05805234A 2005-03-31 2005-10-28 Lithiumionenkondensator Active EP1843362B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2005104727A JP4731967B2 (ja) 2005-03-31 2005-03-31 リチウムイオンキャパシタ
PCT/JP2005/019908 WO2006112070A1 (ja) 2005-03-31 2005-10-28 リチウムイオンキャパシタ

Publications (3)

Publication Number Publication Date
EP1843362A1 EP1843362A1 (de) 2007-10-10
EP1843362A4 EP1843362A4 (de) 2008-08-27
EP1843362B1 true EP1843362B1 (de) 2010-04-21

Family

ID=37114814

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05805234A Active EP1843362B1 (de) 2005-03-31 2005-10-28 Lithiumionenkondensator

Country Status (7)

Country Link
US (1) US7768769B2 (de)
EP (1) EP1843362B1 (de)
JP (1) JP4731967B2 (de)
KR (1) KR101161720B1 (de)
CN (1) CN1954397B (de)
DE (1) DE602005020852D1 (de)
WO (1) WO2006112070A1 (de)

Families Citing this family (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007087714A (ja) * 2005-09-21 2007-04-05 Hitachi Chem Co Ltd エネルギー貯蔵デバイス
KR20090081398A (ko) * 2006-10-17 2009-07-28 맥스웰 테크놀러지스 인코포레이티드 에너지 저장 장치를 위한 전극
JP4934607B2 (ja) * 2008-02-06 2012-05-16 富士重工業株式会社 蓄電デバイス
CN101702541B (zh) * 2009-11-09 2011-07-13 南京双登科技发展研究院有限公司 一种超级电容器内部短路修复方法
KR101153625B1 (ko) * 2010-06-08 2012-06-18 삼성전기주식회사 2차 전원용 전극 제조 방법 및 이를 이용한 2차 전원의 제조 방법
KR101101546B1 (ko) * 2010-06-21 2012-01-02 삼성전기주식회사 전기 화학 커패시터 및 이의 제조방법
JP5682854B2 (ja) * 2010-09-24 2015-03-11 日新電機株式会社 電気二重層キャパシタの製造方法
US20140217322A1 (en) * 2011-02-03 2014-08-07 Jsr Corporation Lithium ion capacitor
JP5840429B2 (ja) * 2011-09-12 2016-01-06 Fdk株式会社 リチウムイオンキャパシタ
DK2794475T3 (da) 2011-12-21 2020-04-27 Univ California Forbundet korrugeret carbonbaseret netværk
ES2934222T3 (es) 2012-03-05 2023-02-20 Univ California Condensador con electrodos hechos de una red a base de carbono corrugado interconectado
JP6100473B2 (ja) 2012-04-10 2017-03-22 Necトーキン株式会社 電気化学デバイス
CN103680972B (zh) * 2012-09-10 2016-08-03 中国科学院金属研究所 一种高能量高功率密度的锂离子超级电容器及其组装方法
JP6262432B2 (ja) * 2013-01-25 2018-01-17 旭化成株式会社 リチウムイオンキャパシタの製造方法
JP2014183161A (ja) * 2013-03-19 2014-09-29 Sumitomo Electric Ind Ltd リチウムイオンキャパシタおよびその充放電方法
CN105723483B (zh) 2013-11-19 2019-09-13 旭化成株式会社 非水系锂型蓄电元件
KR102443607B1 (ko) 2014-06-16 2022-09-16 더 리전트 오브 더 유니버시티 오브 캘리포니아 하이브리드 전기화학 전지
TWI559607B (zh) 2014-07-09 2016-11-21 Asahi Chemical Ind Non - water lithium - type power storage components
ES2935063T3 (es) 2014-11-18 2023-03-01 Univ California Material compuesto poroso interconectado de red corrugada a base de carbono (ICCN)
IL259749B (en) 2015-12-22 2022-08-01 Univ California Thin cellular graphene
CN108475584B (zh) * 2016-01-22 2019-07-02 旭化成株式会社 非水系锂型蓄电元件
EP3352188B1 (de) * 2016-01-22 2020-07-29 Asahi Kasei Kabushiki Kaisha Wasserfreies speicherelement vom lithiumtyp
CA3009208A1 (en) * 2016-01-22 2017-07-27 The Regents Of The University Of California High-voltage devices
US11107639B2 (en) 2016-01-22 2021-08-31 Asahi Kasei Kabushiki Kaisha Positive electrode precursor
JP6975429B2 (ja) 2016-03-23 2021-12-01 ザ リージェンツ オブ ザ ユニバーシティ オブ カリフォルニアThe Regents Of The University Of California 高電圧用及び太陽電池用の装置及び方法
JP6429820B2 (ja) * 2016-03-24 2018-11-28 太陽誘電株式会社 電気化学デバイス
JP2017183539A (ja) * 2016-03-30 2017-10-05 太陽誘電株式会社 電気化学デバイス
JP2019517130A (ja) 2016-04-01 2019-06-20 ザ リージェンツ オブ ザ ユニバーシティ オブ カリフォルニア 柔軟性があり高性能なスーパーキャパシタのための炭素布上でのポリアニリンナノチューブの直接的成長
US11097951B2 (en) 2016-06-24 2021-08-24 The Regents Of The University Of California Production of carbon-based oxide and reduced carbon-based oxide on a large scale
US10938021B2 (en) 2016-08-31 2021-03-02 The Regents Of The University Of California Devices comprising carbon-based material and fabrication thereof
CN109923699B (zh) * 2016-11-07 2022-03-15 日产自动车株式会社 锂离子电池用负极和锂离子电池
KR102563188B1 (ko) 2017-07-14 2023-08-02 더 리전트 오브 더 유니버시티 오브 캘리포니아 슈퍼 커패시터 적용을 위한 탄소 나노 입자로부터 고전도성의 다공성 그래핀으로의 단순 루트
WO2019180971A1 (ja) * 2018-03-23 2019-09-26 三菱電機株式会社 モータ駆動装置、電動送風機、電気掃除機及びハンドドライヤ
CN113950756B (zh) * 2019-06-03 2024-01-02 武藏能源解决方案有限公司 蓄电装置以及锂离子二次电池的制造方法
US10938032B1 (en) 2019-09-27 2021-03-02 The Regents Of The University Of California Composite graphene energy storage methods, devices, and systems

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2719161B1 (fr) * 1994-04-22 1996-08-02 Accumulateurs Fixes Générateur électrochimique rechargeable au lithium à anode de carbone.
US5953204A (en) * 1994-12-27 1999-09-14 Asahi Glass Company Ltd. Electric double layer capacitor
JP3485935B2 (ja) 1997-01-27 2004-01-13 カネボウ株式会社 有機電解質電池
JP3800799B2 (ja) * 1998-04-10 2006-07-26 三菱化学株式会社 電気二重層キャパシター
JP4412778B2 (ja) * 1999-01-20 2010-02-10 三洋電機株式会社 ポリマー電解質電池
JP4601752B2 (ja) * 1999-09-30 2010-12-22 ソニー株式会社 ゲル状電解質及びゲル状電解質電池
JP4608735B2 (ja) * 2000-05-16 2011-01-12 ソニー株式会社 非水電解質二次電池の充電方法
KR100473433B1 (ko) * 2000-07-17 2005-03-08 마쯔시다덴기산교 가부시키가이샤 비수전해액 및 그것을 포함하는 비수전해액전지 및 전해콘덴서
JP4843834B2 (ja) * 2000-07-17 2011-12-21 パナソニック株式会社 非水電解質二次電池
EP1239495B1 (de) * 2001-03-09 2006-08-09 Asahi Glass Company Ltd. Sekundär-Energiequelle
WO2002093679A1 (fr) * 2001-05-10 2002-11-21 Nisshinbo Industries, Inc. Solution electrolytique non aqueuse, composition pour electrolyte en gel polymere, electrolyte en gel polymere, accumulateur, et condensateur electrique forme de deux couches
CA2451634C (en) * 2001-06-29 2009-06-30 Kanebo, Limited Organic electrolytic capacitor
JP2004111349A (ja) * 2002-07-23 2004-04-08 Central Glass Co Ltd 電気化学ディバイスの溶媒分解抑制方法及びそれを用いた電気化学ディバイス
JP2004221425A (ja) * 2003-01-16 2004-08-05 Tdk Corp 電極及びその製造方法、並びに、電気化学素子、電気化学キャパシタ、電池、及び電気化学センサ

Also Published As

Publication number Publication date
US7768769B2 (en) 2010-08-03
EP1843362A4 (de) 2008-08-27
CN1954397A (zh) 2007-04-25
DE602005020852D1 (de) 2010-06-02
JP4731967B2 (ja) 2011-07-27
KR20070108808A (ko) 2007-11-13
WO2006112070A1 (ja) 2006-10-26
JP2006286924A (ja) 2006-10-19
US20090174986A1 (en) 2009-07-09
EP1843362A1 (de) 2007-10-10
KR101161720B1 (ko) 2012-07-03
CN1954397B (zh) 2010-05-05

Similar Documents

Publication Publication Date Title
EP1843362B1 (de) Lithiumionenkondensator
EP1895553B1 (de) Lithiumionenkondensator
KR101127326B1 (ko) 리튬이온 커패시터
US7817403B2 (en) Lithium ion capacitor
KR100863562B1 (ko) 유기 전해질 커패시터
EP1400996B1 (de) Kondensator mit organischem elektrolyt
EP1865520B1 (de) Lithiumionenkondensator
US7733629B2 (en) Lithium ion capacitor
KR101045159B1 (ko) 리튬이온 커패시터
KR101573106B1 (ko) 권회형 축전지
JP2006286919A (ja) リチウムイオンキャパシタ
KR20080081297A (ko) 리튬이온 커패시터
JP2006286926A (ja) リチウムイオンキャパシタ
JP5027540B2 (ja) リチウムイオンキャパシタ
JP2008166309A (ja) リチウムイオンキャパシタ
JP2008060479A (ja) リチウムイオンキャパシタ
JP2007180434A (ja) リチウムイオンキャパシタ
JP2008071975A (ja) リチウムイオンキャパシタ
JP2007180437A (ja) リチウムイオンキャパシタ
JP2006286921A (ja) リチウムイオンキャパシタ

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20060330

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): DE FR GB NL

DAX Request for extension of the european patent (deleted)
RBV Designated contracting states (corrected)

Designated state(s): DE FR GB NL

A4 Supplementary search report drawn up and despatched

Effective date: 20080724

17Q First examination report despatched

Effective date: 20080922

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): DE FR GB NL

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REF Corresponds to:

Ref document number: 602005020852

Country of ref document: DE

Date of ref document: 20100602

Kind code of ref document: P

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20100421

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100421

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed

Effective date: 20110124

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20101028

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20101028

REG Reference to a national code

Ref country code: FR

Ref legal event code: CA

Effective date: 20141124

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 12

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 602005020852

Country of ref document: DE

Representative=s name: MUELLER-BORE & PARTNER PATENTANWAELTE PARTG MB, DE

Ref country code: DE

Ref legal event code: R081

Ref document number: 602005020852

Country of ref document: DE

Owner name: SUBARU CORPORATION, JP

Free format text: FORMER OWNER: FUJI JUKOGYO K.K., TOKIO/TOKYO, JP

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 13

REG Reference to a national code

Ref country code: FR

Ref legal event code: CD

Owner name: SUBARU CORPORATION, JP

Effective date: 20171114

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 14

REG Reference to a national code

Ref country code: DE

Ref legal event code: R084

Ref document number: 602005020852

Country of ref document: DE

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20231023

Year of fee payment: 19

Ref country code: DE

Payment date: 20231020

Year of fee payment: 19